EP3915758A1 - Schnecke und extruder - Google Patents

Schnecke und extruder Download PDF

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Publication number
EP3915758A1
EP3915758A1 EP19917405.3A EP19917405A EP3915758A1 EP 3915758 A1 EP3915758 A1 EP 3915758A1 EP 19917405 A EP19917405 A EP 19917405A EP 3915758 A1 EP3915758 A1 EP 3915758A1
Authority
EP
European Patent Office
Prior art keywords
region
screw
elastomer
kneading
spiral blade
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP19917405.3A
Other languages
English (en)
French (fr)
Other versions
EP3915758A4 (de
Inventor
Tadasuke Sato
Noriyuki Takeda
Makoto Noda
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nakata Engineering Co Ltd
Original Assignee
Nakata Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nakata Engineering Co Ltd filed Critical Nakata Engineering Co Ltd
Publication of EP3915758A1 publication Critical patent/EP3915758A1/de
Publication of EP3915758A4 publication Critical patent/EP3915758A4/de
Pending legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
    • B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
    • B29B7/422—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix with screw sections co-operating, e.g. intermeshing, with elements on the wall of the surrounding casing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
    • B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
    • B29B7/421—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix with screw and additionally other mixing elements on the same shaft, e.g. paddles, discs, bearings, rotor blades of the Banbury type
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
    • B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
    • B29B7/428—Parts or accessories, e.g. casings, feeding or discharging means
    • B29B7/429—Screws
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/285—Feeding the extrusion material to the extruder
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/505—Screws
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/505—Screws
    • B29C48/565—Screws having projections other than the thread, e.g. pins
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/505—Screws
    • B29C48/59—Screws characterised by details of the thread, i.e. the shape of a single thread of the material-feeding screw
    • B29C48/605—Screws characterised by details of the thread, i.e. the shape of a single thread of the material-feeding screw the thread being discontinuous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/505—Screws
    • B29C48/64—Screws with two or more threads
    • B29C48/645—Screws with two or more threads neighbouring threads and channels having identical configurations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/505—Screws
    • B29C48/64—Screws with two or more threads
    • B29C48/66—Barrier threads, i.e. comprising primary and secondary threads whereby the secondary thread provides clearance to the barrel for material movement
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/68—Barrels or cylinders
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/68—Barrels or cylinders
    • B29C48/6801—Barrels or cylinders characterised by the material or their manufacturing process
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/68—Barrels or cylinders
    • B29C48/681—Barrels or cylinders for single screws
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/68—Barrels or cylinders
    • B29C48/685—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/68—Barrels or cylinders
    • B29C48/685—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads
    • B29C48/687—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads having projections with a short length in the barrel direction, e.g. pins
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2021/00—Use of unspecified rubbers as moulding material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2021/00—Use of unspecified rubbers as moulding material
    • B29K2021/003—Thermoplastic elastomers

Definitions

  • the present invention relates to a screw and an extruder for extruding a plastic elastomer while kneading.
  • Patent Document 1 discloses a pin-type extruder which includes a screw arranged in the barrel and a plurality of pins protruding from the inner peripheral surface of the barrel toward the screw.
  • Patent Document 1 Japanese Unexamined Patent Application Publication H02-137908
  • the present invention has been made in view of the above circumstance, and has a major object to provide a screw and an extruder capable of stabilizing the shape of plastic elastomers after extrusion by reducing expansion coefficient thereof.
  • the present invention includes a screw with a spiral blade for extruding a plastic elastomer while kneading the plastic elastomer, the screw including, a kneading region where the spiral blade is provided with cutout portions being configured to pass pins, and a plasticizing region being arranged on a downstream side in an extrusion direction of the kneading region, wherein the plasticizing region comprises a barrier extending between portions adjacently in the extrusion direction of the spiral blade.
  • the plasticizing region includes three to six barriers.
  • the barrier has a height smaller than a height of the spiral blade and a difference (D) between the heights is equal to or less than 4 mm.
  • the barrier has a thickness (t) equal to or more than 1.5 times of the difference (D) of the heights.
  • a feed region is arranged on an upstream side in the extrusion direction of the kneading region, wherein the spiral blade of the feed region is formed into a single thread.
  • the spiral blade of the kneading region and the plasticizing region is formed into a double thread.
  • the present invention includes an extruder comprising a screw as set forth above and a barrel in which the screw is disposed, wherein the barrel comprises a plurality of pins that passes the cutout portions of the spiral blade of the kneading promoting region.
  • the barrel further includes an inlet for introducing the elastomer, wherein the inlet supplies the elastomer to a feed region that is located on an upstream side in the extrusion direction of the kneading region.
  • the screw according to the present invention includes a kneading region in which cutout portions for passing pins are formed in the spiral blade, and a plasticizing region being arranged on a downstream side in the extrusion direction of the kneading region, wherein the plasticizing region has a barrier extending between portions adjacently in the extrusion direction of the spiral blade.
  • the kneading region as with a pin-type extruder, can knead and shear the elastomer between the screw and the barrel by pins passing through the cutout portions. Moreover, in the kneading region, the resistance between the barrel and the elastomer increases, and thus the kneading effect also increases, resulting in enhancing mixing and dispersion effect.
  • the elastomer that passes between the adjacent portions of the spiral blade flows downstream while overcoming the barrier. After overcoming, the elastomer deforms into a thin film. At that time, the elastomer deforms in the shearing direction and the pulling direction, and the molecules are cut uniformly and finely. In this way, in the plasticizing region, the effect of cutting elastomer molecules is highly exhibited. Thus, the expansion coefficient of the elastomer after extrusion can be reduced, and the shape thereof can be stabilized.
  • the elastomer when the elastomer is deformed into a thin film, the elastomer itself generates heat and warming effect is improved. As a result, the mixing and dispersion of additives are promoted in combination with the cutting effect of the molecule. Thus, it can contribute to the improvement of surface properties such as smoothing the surface properties of the extruded elastomer.
  • FIG. 1 is a side view of an extruder 1 according to an embodiment.
  • the extruder 1 according to the present embodiment includes a screw 2 for extruding a plastic elastomer G while kneading the same in an extrusion direction A, and a barrel 3 in which the screw 2 is disposed.
  • the plastic elastomer G for example, unvulcanized rubber, thermoplastic elastomer, etc. can be applied.
  • the screw 2 includes a screw main shaft 4 and a spiral blade 5 that protrudes outwardly in the radial direction of the screw 2 from the screw main shaft 4.
  • the spiral blade 5 is for extruding the elastomer G while kneading the same, and is formed as a single thread, a double thread screw, or a multi thread.
  • a single thread has an aspect in which one spiral blade 5 is provided at an axial region of the screw main shaft 4.
  • a double thread has an aspect in which the screw main shaft 4 has two spiral blades 5 in an axial region.
  • a multi thread has an aspect in which the screw main shaft 4 has two or more spiral blades 5 in an axial region.
  • a double thread is one aspect of a multi thread.
  • FIG. 2 is a side view of the screw 2 shown in FIG. 1 .
  • the screw 2 includes a kneading region 6, and a plasticizing region 7 arranged on a downstream side in the extrusion direction A of the kneading region 6.
  • a feed region 8 is further arranged on the upstream side in the extrusion direction A of the kneading region 6.
  • the spiral blade 5 of the feed region 8 is preferably formed into a single thread. Further, the spiral blade 5 of the kneading region 6 and the plasticizing region 7 is preferably formed into a multi thread, especially a double thread.
  • cutout portions 10 for passing pins are formed in the spiral blade 5.
  • four cutout portions 10 are provided on the spiral blade 5.
  • the number of the cutout portions 10 is not limited to this, but can be modified appropriately depending on the type of elastomer G.
  • Such a kneading region 6 can shear the elastomer G between the screw 2 and the barrel 3 by the spiral blade 5 and pins 10 passing through the cutout portions 10. Moreover, in the kneading region 6, the resistance between the barrel 3 and the elastomer G increases, and thus the kneading effect also increases, resulting in enhancing mixing and dispersion effect.
  • the plasticizing region 7 includes one or more barriers 14 extending between portions adjacently in the extrusion direction A of the spiral blade 5.
  • a height of the barriers 14 is smaller than a height of the spiral blade 5.
  • the elastomer G overcomes the barriers 14 and flows downstream of the extrusion direction A while deforming into a thin film.
  • the elastomer G deforms in the shearing direction and the pulling direction, and the molecules are cut uniformly and finely. That is, in the plasticizing region 7, the effect of cutting the molecule of the elastomer G is highly exhibited.
  • the expansion coefficient of the elastomer G after extrusion can be reduced, and the stabilization of the shape after extrusion is possible.
  • the elastomer G when the elastomer G is deformed into a thin film, the elastomer itself generates heat and warming effect is improved. As a result, the mixing and dispersion of additives are promoted in combination with the cutting effect of the molecule. Thus, it can contribute to the improvement of surface properties such as smoothing the surface properties of the extruded elastomer.
  • the difference D between the height of the barriers 14 and the height of the spiral blade 5 is equal to or less than 4 mm.
  • the difference D of the heights exceeds 4 mm, deformation to a thin film is insufficient and the effect of cutting molecules may be reduced.
  • the upper limit of the difference D of the heights is 3 mm or less.
  • the lower limit of the difference D of the heights is preferably equal to or more than 1 mm. When it is less than 1 mm, the flow is hindered and the discharge amount of the elastomer G decreases.
  • a thickness t of the barriers 14 is 1.5 times or more of the difference D of the heights. If the thickness t is less than 1.5 times of the difference D of the heights, deformation of molecule of the elastomer G in the tensile direction becomes insufficient when passing over the barriers 14, which tends to reduce the cutting effect.
  • the upper limit of the thickness t is preferably equal to or less than 10.0 times of the difference D of the heights. If it exceeds 10.0 times, the flow is hindered and the discharge amount of the elastomer G decreases.
  • the number of the barriers 14 formed in the plasticizing region 7 is preferably in a range of three to six from the viewpoint of the effect of reducing the expansion coefficient and the reduction of the discharge amount.
  • a lead angle ⁇ of the barriers 14 is not specified and can be set appropriately in a range of 0 to 90 degrees.
  • the elastomer G will be difficult to overcome the barriers 14 having the difference D of the heights being 4 mm or less, which will be difficult to obtain a sufficient effect of reducing the expansion coefficient.
  • the discharge amount is greatly reduced. That is, the synergistic action of the kneading region 6 and the plasticizing region 7 makes it possible to sufficiently obtain the effect of reducing the expansion coefficient without causing a large decrease in the discharge amount.
  • the barrel 3 for example, is formed into a substantially cylindrical shape with a substantially constant inner diameter.
  • the barrel 3 includes an inlet 11 for introducing the elastomer G and a discharge port 12 for discharging kneaded the elastomer G.
  • the inlet 11 is located in the feed region 8, and the elastomer G is supplied from the inlet 11 into the feed region 8.
  • the spiral blade 5 since the spiral blade 5 is formed into a single thread, it exhibits excellent biting property with respect to the supplied elastomer G. This may ensure that the elastomer G is not overflowed from the inlet 11 and is surely sent into the barrel 3.
  • the barrel 3 includes a plurality of pins 13 which can pass through the cutout portions 10 provided in the spiral blade 5 of the kneading region 6.
  • the barrel 3 includes a plurality of pins 13 (e.g., four to eight) that passes through each cutout portion 10 of the spiral blade 5.
  • the pins 13 are arranged in multiple rows (e.g., three to five rows) in the extrusion direction A. Such pins 13 can shear the elastomer G kneaded between the screw 2 and the barrel 3.
  • the pins 13 increase resistance between the barrel 3 and the elastomer G, which can enhance kneading effect and mixing and dispersing effect. It is preferable that a protruding amount of the pins 13 into the barrel 3 can be modified as appropriate.
  • the screw 2 is rotated in one direction by a drive unit 15 arranged on the upstream side of the extrusion direction A of the barrel 3.
  • the rotation speed of the screw 2 can be adjusted as appropriate by the drive unit 15.
  • Such a screw 2 can easily change the rotation speed according to the operating conditions of the extruder 1.
  • the screw 2 has an extrusion region 9 in which the spiral blade 5 is formed into a double threaded on the downstream side of the extrusion direction A of the plasticizing region 7. In this way, the extrusion region 9 can stably discharge the elastomer G from the discharge port 12 of the barrel 3.
  • extruders having the structure shown in FIG. 1 and having a Gervey die at the front end was constructed. Then, the extruders were operated at the same rotation speed and the same temperature conditions with each other. The coefficient of expansion, plasticity, surface properties of the extruded material, and discharge amount of the elastomer G after extrusion were measured and compared with the conventional and comparative examples. As a conventional example, a pin extruder was used.
  • elastomer 50 parts by weight of carbon black and 5 parts by weight of oil were mixed with 100 parts by weight of natural rubber.
  • Mooney viscosity (1+4) at 130 deg. C was measured and shown as an index with the conventional example as 100. The smaller the value, the better the plasticity is.
  • the surface roughness (arithmetic mean roughness Ra) of the molded product extruded from the discharge port was measured. The smaller the value, the smoother the surface is.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
EP19917405.3A 2019-02-25 2019-11-28 Schnecke und extruder Pending EP3915758A4 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2019031491A JP6949891B2 (ja) 2019-02-25 2019-02-25 スクリュー及び押出機
PCT/JP2019/046526 WO2020174793A1 (ja) 2019-02-25 2019-11-28 スクリュー及び押出機

Publications (2)

Publication Number Publication Date
EP3915758A1 true EP3915758A1 (de) 2021-12-01
EP3915758A4 EP3915758A4 (de) 2022-10-26

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP19917405.3A Pending EP3915758A4 (de) 2019-02-25 2019-11-28 Schnecke und extruder

Country Status (7)

Country Link
US (1) US20220080620A1 (de)
EP (1) EP3915758A4 (de)
JP (1) JP6949891B2 (de)
KR (1) KR20210113674A (de)
CN (1) CN113412182A (de)
TW (1) TW202031457A (de)
WO (1) WO2020174793A1 (de)

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KR20210113674A (ko) 2021-09-16
JP6949891B2 (ja) 2021-10-13
EP3915758A4 (de) 2022-10-26
US20220080620A1 (en) 2022-03-17
CN113412182A (zh) 2021-09-17
JP2020131656A (ja) 2020-08-31
TW202031457A (zh) 2020-09-01

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